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Steam loss tables for Radiator and Flow traps


Steam loss table for Radiator traps Back to the top...

Pressure-balanced Thermostatic Radiator traps are most commonly found on low pressure (25 psig and under) steam heating systems. Located on radiators, convectors and other radiant heat units, there may be literally hundreds of these scattered throughout larger facilities. The operating unit within the trap - a pressure-balanced disc or bellows - is filled with a distilled liquid to respond to the changes in temperature (i.e. pressure) within the trap.


 Steam cost at £4.00/1000 lbs

The disc or bellows will generally 'fail open' after three to five years of hard work (after five years, it has opened and closed hundreds of thousands of times). The orifice sizes (*) shown for all the steam traps are conservative estimates of the average size found in these traps. Actual loss may be more or less than shown.

Pressure at trap 2 PSIG 5 PSIG 10 PSIG 15 PSIG 25 PSIG
Pipe size 1/2" *1/4* *1/4* *1/4* *1/4* *1/4*
Loss per month £15 £21 £27 £32 £43
Pipe size 3/4" *5/16* *5/16* *5/16* *5/16* *5/16*
Loss per month £23 £33 £42 £51 £67
Pipe size 1" *3/8* *3/8* *3/8* *3/8* *3/8*
Loss per month £32 £48 £61 £73 £97

Pressure at trap 50 PSIG 75 PSIG 100 PSIG 125 PSIG 150 PSIG
Pipe size 1/2" *7/32* *7/32* *7/32* *7/32* *3/16*
Loss per month £54 £75 £95 £117 £101
Pipe size 3/4" *1/4* *1/4* *1/4* *1/4* *7/32*
Loss per month £71 £98 £124 £152 £137
Pipe size 1" *5/16* *5/16* *5/16* *5/16* *9/32*
Loss per month £110 £153 £196 £238 £227

* Assigned orifice sizes employed in the traps when under the differential operating pressures as shown.


Steam loss table for Float and Thermostatic traps Back to the top...

Float and Thermostatic (F&T) traps are found where higher levels of condensate are produced - such as unit heaters, end-of-mains, heat exchangers, etc. The modulating control provided by the float allows for continuous discharge of condensate when necessary. The air vent in this trap will generally "fail open" after three to five years of hard work.


 Steam cost at £4.00/1000 lbs

The mechanism and float assembly, which allows the condensate to discharge, may operate efficiently for eight to ten years, and will normally "fail closed" after this time. However, sludge and debris accumulation may cause the assembly to fail open and waste a lot of money as shown below. Actual pound loss may vary.

Pressure at trap 2 PSIG 5 PSIG 10 PSIG 15 PSIG 25 PSIG
Pipe size 3/4" & 1" *1/4* *1/4* *1/4* *1/4* *3/16*
Loss per month £15 £21 £27 £32 £25
Pipe size 1 1/4" *5/16* *5/16* *5/16* *5/16* *1/4*
Loss per month £23 £33 £42 £51 £43
Pipe size 1 1/2" *3/32* *3/32* *3/32* *3/32* *5/16*
Loss per month £38 £57 £70 £86 £67
Pipe size 2" *1/2* *1/2* *1/2* *1/2* *5/32*
Loss per month £57 £86 £108 £129 £152

* Assigned orifice sizes employed in the traps when under the differential operating pressures as shown.

Pressure at trap 50 PSIG 75 PSIG> 100 PSIG 125 PSIG 150 PSIG
Pipe size 3/4" & 1" *1/8* *1/8* *3/32* *3/32* *3/32*
Loss per month £17 £25 £17 £21 £25
Pipe size 1 1/4" *3/16* *3/16* *1/8* *1/8* *1/8*
Loss per month £40 £55 £31 £38 £45
Pipe size 1 1/2" *7/32* *7/32* *5/32* *5/32* *5/32*
Loss per month £54 £75 £49 £59 £70
Pipe size 2" *7/16* *7/16* *5/16* *5/16* *5/16*
Loss per month £216 £344 £196 £238 £281

* Assigned orifice sizes employed in the traps when under the differential operating pressures as shown.


 The air vents in all the F&T traps generally utilise a 1/4" discharge orifice

Contact us Back to the top...

Should you have any questions, or if you would like to discuss any of this further, then please do not hesitate to get in touch.


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Our thanks to Alastair Hazell Back to the top...